Process for preparing esters of lactic acid, and 2-hydroxy-3-butenoic acid or α-hydroxy methionine analogues from sugars

US10100007B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10100007-B2
Application numberUS-201515525450-A
CountryUS
Kind codeB2
Filing dateNov 12, 2015
Priority dateNov 28, 2014
Publication dateOct 16, 2018
Grant dateOct 16, 2018

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

A continuous flow process for the preparation of one or more esters of lactic acid and 2-hydroxy-3-butenoic acid or α-hydroxy methionine analogs from a sugar in the presence of a solid Lewis acid catalyst and a solvent comprising an organic solvent and water. The invention provides a means for stabilizing a Lewis acid catalyst for use in a continuous reaction process wherein the water is present in an amount of up to or equal to 10 vol. % of the organic solvent.

First claim

Opening claim text (preview).

The invention claimed is: 1. A continuous flow process for the preparation of one or more esters of lactic acid and 2-hydroxy-3-butenoic acid from a sugar selected from one or more of the group consisting of glucose, fructose, mannose, sucrose, xylose, erythrose, erythrulose, threose and glycolaldehyde, in the presence of a solid Lewis acid catalyst and a solvent comprising an organic solvent and water, wherein the water is present in an amount of up to or equal to 10 vol. % of the organic solvent, wherein the solid Lewis acid catalyst has a framework structure, which is selected from the group consisting of BEA, MFI, FAU, MOR, FER, MWW, MCM-41 and SBA-15. 2. A process according to claim 1 , wherein the yield of the one or more lactic acid esters decreases by up to 0.25% per hour on stream on average, wherein the yield is amount of ester relative to the amount of sugar. 3. A process according to claim 1 , wherein the yield of the one or more lactic acid esters decreases by up to 0.10% per hour on average, wherein the yield is amount of ester relative to the amount of sugar. 4. A process according to claim 1 , wherein the yield of the one or more lactic acid esters decreases by up to 5% after 50 hours on stream, wherein the yield is amount of ester relative to the amount of sugar. 5. A process according to claim 1 , wherein the yield of the one or more lactic acid esters is greater than 40% after 50 hours on stream, wherein the yield is amount of ester relative to the amount of sugar. 6. A process according to claim 1 , wherein the solid Lewis acid catalyst is calcined after 450 hours of continuous flow process. 7. A process according to claim 1 , wherein the solid Lewis acid catalyst comprises an active metal selected from one or more of the group consisting of Sn, Ti, Pb, Zr, Ge and Hf. 8. A process according to claim 1 , wherein the solid Lewis acid catalyst is selected from the group consisting of Sn-BEA, Sn-MFI, Sn-FAU, Sn-MOR, Sn-MWW, Sn-MCM-41 and Sn-SBA-15. 9. A process according to claim 1 , wherein the solid Lewis acid catalyst comprises Sn and the loss of Sn from the solid Lewis acid catalyst is less than or equal to 0.11% of the initial amount of Sn per hour on stream. 10. A process according to claim 1 , wherein the solid Lewis acid catalyst comprises Sn and the loss of Sn from the solid Lewis acid catalyst is less than 8% of the initial amount of Sn after 50 hours on stream. 11. A process according to claim 1 , wherein the yield of 2-hydroxy-3-butenoic acid ester is greater than 12% after 50 hours on stream, wherein the yield is amount of ester relative to the amount of sugar. 12. A process according to claim 1 , wherein an alkaline earth metal or alkali metal ion is present in the process. 13. A process according to claim 1 , wherein the solvent is selected from one or more of the group consisting of methanol, ethanol, 1-propanol, 1-butanol and isopropanol. 14. A process according to claim 1 , wherein the temperature of the process is from 140° C. to 200° C. 15. A process according to claim 1 , wherein at least a fraction of the water is introduced to the solvent by mixing the organic solvent with an aqueous sugar solution. 16. A process according to claim 1 , wherein the aqueous sugar solution is a sugar syrup with a sugar dry matter content of 30% or higher.

Assignees

Inventors

Classifications

  • of unsaturated hydroxy carboxylic acids · CPC title

  • by oxidation-reduction of aldehydes, e.g. Tishchenko reaction · CPC title

  • C07C319/18Primary

    by addition of thiols to unsaturated compounds · CPC title

  • by splitting of carbon-to-carbon bonds and redistribution, e.g. disproportionation or migration of [IMAGE cpc-sch-C07C-0963.gif] groups between different molecules · CPC title

  • Lactic acid esters · CPC title

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What does patent US10100007B2 cover?
A continuous flow process for the preparation of one or more esters of lactic acid and 2-hydroxy-3-butenoic acid or α-hydroxy methionine analogs from a sugar in the presence of a solid Lewis acid catalyst and a solvent comprising an organic solvent and water. The invention provides a means for stabilizing a Lewis acid catalyst for use in a continuous reaction process wherein the water is presen…
Who is the assignee on this patent?
Haldor Topsoe As, Haldor Topsoe As
What technology area does this patent fall under?
Primary CPC classification C07C319/18. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Oct 16 2018 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).